BRPI0616497B1 - processo para aumentar a produção de olefinas leves a partir da matéria-prima de hidrocarboneto na destilação fracionada catalítica - Google Patents
processo para aumentar a produção de olefinas leves a partir da matéria-prima de hidrocarboneto na destilação fracionada catalítica Download PDFInfo
- Publication number
- BRPI0616497B1 BRPI0616497B1 BRPI0616497-8A BRPI0616497A BRPI0616497B1 BR PI0616497 B1 BRPI0616497 B1 BR PI0616497B1 BR PI0616497 A BRPI0616497 A BR PI0616497A BR PI0616497 B1 BRPI0616497 B1 BR PI0616497B1
- Authority
- BR
- Brazil
- Prior art keywords
- catalytic
- fractional distillation
- hydrocarbon
- distillation
- production
- Prior art date
Links
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 108
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 102
- 238000000034 method Methods 0.000 title claims abstract description 95
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 87
- 238000004508 fractional distillation Methods 0.000 title claims abstract description 85
- 230000008569 process Effects 0.000 title claims abstract description 85
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 61
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 46
- 150000001336 alkenes Chemical class 0.000 title claims abstract description 45
- 238000004064 recycling Methods 0.000 claims abstract description 29
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims description 52
- 239000003054 catalyst Substances 0.000 claims description 32
- 239000002994 raw material Substances 0.000 claims description 21
- 238000004821 distillation Methods 0.000 claims description 20
- 239000007795 chemical reaction product Substances 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 11
- 239000003350 kerosene Substances 0.000 claims description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- -1 olefin hydrocarbons Chemical class 0.000 claims description 9
- 229910021536 Zeolite Inorganic materials 0.000 claims description 8
- 239000010457 zeolite Substances 0.000 claims description 8
- 230000008033 biological extinction Effects 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 238000011069 regeneration method Methods 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 230000008929 regeneration Effects 0.000 claims description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 3
- 230000000737 periodic effect Effects 0.000 claims description 3
- 238000010791 quenching Methods 0.000 claims description 2
- 230000001172 regenerating effect Effects 0.000 claims description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 230000000171 quenching effect Effects 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 12
- 238000010276 construction Methods 0.000 abstract description 10
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 20
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 13
- 239000005977 Ethylene Substances 0.000 description 13
- 230000000052 comparative effect Effects 0.000 description 13
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 13
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 13
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 11
- 238000005984 hydrogenation reaction Methods 0.000 description 11
- 239000001294 propane Substances 0.000 description 10
- 230000008570 general process Effects 0.000 description 9
- 239000000295 fuel oil Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 238000001256 steam distillation Methods 0.000 description 7
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 239000003502 gasoline Substances 0.000 description 5
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000037361 pathway Effects 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000005243 fluidization Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000004148 unit process Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- CXBDYQVECUFKRK-UHFFFAOYSA-N 1-methoxybutane Chemical group CCCCOC CXBDYQVECUFKRK-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000010960 commercial process Methods 0.000 description 1
- 238000005094 computer simulation Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/06—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/04—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only including only thermal and catalytic cracking steps
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/10—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1051—Kerosene having a boiling range of about 180 - 230 °C
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4081—Recycling aspects
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
- C10G2300/805—Water
- C10G2300/807—Steam
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2005-0094467 | 2005-10-07 | ||
| KR1020050094467A KR100632571B1 (ko) | 2005-10-07 | 2005-10-07 | 탄화수소 원료 혼합물로부터 접촉분해공정을 통해서 경질올레핀계 탄화수소 화합물을 증산하는 방법 |
| PCT/KR2006/001880 WO2007043738A1 (fr) | 2005-10-07 | 2006-05-19 | Procede permettant d'augmenter la production d'olefines legeres a partir d'une charge d'hydrocarbures en craquage catalytique |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| BRPI0616497A2 BRPI0616497A2 (pt) | 2012-12-25 |
| BRPI0616497B1 true BRPI0616497B1 (pt) | 2015-09-08 |
Family
ID=37635514
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BRPI0616497-8A BRPI0616497B1 (pt) | 2005-10-07 | 2006-05-19 | processo para aumentar a produção de olefinas leves a partir da matéria-prima de hidrocarboneto na destilação fracionada catalítica |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US7939702B2 (fr) |
| EP (1) | EP1931611A4 (fr) |
| JP (1) | JP5293954B2 (fr) |
| KR (1) | KR100632571B1 (fr) |
| CN (1) | CN101228104B (fr) |
| BR (1) | BRPI0616497B1 (fr) |
| CA (1) | CA2617887C (fr) |
| RU (1) | RU2416594C2 (fr) |
| WO (1) | WO2007043738A1 (fr) |
Families Citing this family (44)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7892418B2 (en) | 2005-04-11 | 2011-02-22 | Oil Tech SARL | Process for producing low sulfur and high cetane number petroleum fuel |
| US8608942B2 (en) * | 2007-03-15 | 2013-12-17 | Kellogg Brown & Root Llc | Systems and methods for residue upgrading |
| KR100904297B1 (ko) * | 2007-10-26 | 2009-06-25 | 한국화학연구원 | 연속적인 2단계 촉매 반응을 이용한 합성가스로부터 경질올레핀의 제조방법 |
| US7883618B2 (en) * | 2008-02-28 | 2011-02-08 | Kellogg Brown & Root Llc | Recycle of olefinic naphthas by removing aromatics |
| CN101323798B (zh) * | 2008-07-31 | 2012-10-31 | 石宝珍 | 一种催化转化方法及其专用装置 |
| US8137631B2 (en) * | 2008-12-11 | 2012-03-20 | Uop Llc | Unit, system and process for catalytic cracking |
| US8246914B2 (en) * | 2008-12-22 | 2012-08-21 | Uop Llc | Fluid catalytic cracking system |
| US8889076B2 (en) * | 2008-12-29 | 2014-11-18 | Uop Llc | Fluid catalytic cracking system and process |
| FR2959748B1 (fr) * | 2010-05-06 | 2012-05-18 | Inst Francais Du Petrole | Procede de craquage catalytique avec recycle d'une coupe olefinique prelevee en amont de la section de separation des gaz afin de maximiser la production de propylene. |
| US20120041243A1 (en) * | 2010-08-10 | 2012-02-16 | Uop Llc | Integration of a methanol-to-olefin reaction system with a hydrocarbon pyrolysis system |
| CN102465001A (zh) * | 2010-11-17 | 2012-05-23 | 中国石油化工股份有限公司 | 石脑油催化转化为低碳烯烃的方法 |
| US9181146B2 (en) | 2010-12-10 | 2015-11-10 | Exxonmobil Chemical Patents Inc. | Process for the production of xylenes and light olefins |
| US8921633B2 (en) | 2012-05-07 | 2014-12-30 | Exxonmobil Chemical Patents Inc. | Process for the production of xylenes and light olefins |
| WO2013169462A1 (fr) * | 2012-05-07 | 2013-11-14 | Exxonmobil Chemical Patents Inc. | Procédé de production de xylènes et d'oléfines légères |
| US9181147B2 (en) | 2012-05-07 | 2015-11-10 | Exxonmobil Chemical Patents Inc. | Process for the production of xylenes and light olefins |
| US8937205B2 (en) | 2012-05-07 | 2015-01-20 | Exxonmobil Chemical Patents Inc. | Process for the production of xylenes |
| JP6181181B2 (ja) * | 2012-08-09 | 2017-08-16 | リンデ アクチエンゲゼルシャフトＬｉｎｄｅ Ａｋｔｉｅｎｇｅｓｅｌｌｓｃｈａｆｔ | 分解炉における熱水蒸気分解によってオレフィンを製造する方法 |
| WO2014023418A1 (fr) * | 2012-08-09 | 2014-02-13 | Linde Aktiengesellschaft | Procédé de fabrication d'oléfines par craquage thermique à la vapeur d'eau |
| US9745519B2 (en) | 2012-08-22 | 2017-08-29 | Kellogg Brown & Root Llc | FCC process using a modified catalyst |
| CN103739418B (zh) * | 2012-10-17 | 2016-07-13 | 中国石油化工股份有限公司 | 提高甲醇制低碳烯烃工艺中低碳烯烃收率的方法 |
| US9428695B2 (en) | 2013-02-12 | 2016-08-30 | Saudi Basic Industries Corporation | Conversion of plastics to olefin and aromatic products with product recycle |
| US8895790B2 (en) * | 2013-02-12 | 2014-11-25 | Saudi Basic Industries Corporation | Conversion of plastics to olefin and aromatic products |
| CN105163851A (zh) | 2013-04-29 | 2015-12-16 | 沙特基础工业公司 | 石脑油转化成烯烃的催化方法 |
| KR102318318B1 (ko) * | 2013-06-04 | 2021-10-28 | 유오피 엘엘씨 | 나프타 분해 |
| US9328299B2 (en) | 2013-06-04 | 2016-05-03 | Uop Llc | Naphtha cracking |
| US9328298B2 (en) | 2013-06-04 | 2016-05-03 | Uop Llc | Naphtha cracking |
| CN104557377B (zh) * | 2013-10-28 | 2018-07-13 | 中国石油化工股份有限公司 | 含氧化合物与石脑油耦合反应生产乙烯与丙烯的方法 |
| CN104628507B (zh) * | 2013-11-06 | 2018-06-08 | 中国石油化工股份有限公司 | 由甲醇制备低碳烯烃的方法 |
| CN105349172B (zh) * | 2014-08-20 | 2017-03-01 | 中国石油化工股份有限公司 | 石脑油原料的催化裂解方法 |
| US11001772B2 (en) * | 2016-02-29 | 2021-05-11 | Sabic Global Technologies B.V. | Process for producing olefins using aromatic saturation |
| IL261271B2 (en) | 2016-03-02 | 2025-03-01 | Agrimetis Llc | Methods for preparing L-glucosinate |
| WO2018069794A1 (fr) | 2016-10-11 | 2018-04-19 | Sabic Global Technologies, B.V. | Maximisation de produits chimiques à valeur élevée à partir de plastique mixte à l'aide de différentes configurations de vapocraqueur |
| JP6956187B2 (ja) | 2017-01-05 | 2021-11-02 | サビック グローバル テクノロジーズ ベスローテン フェンノートシャップ | 廃棄プラスチックのプロピレンおよびクメンへの変換 |
| EP3565799B1 (fr) | 2017-01-05 | 2020-10-07 | SABIC Global Technologies B.V. | Conversion de déchets plastiques en propylène et cumène |
| CN111479905B (zh) * | 2017-12-15 | 2023-09-01 | 沙特基础全球技术有限公司 | 用于在石脑油催化裂化工艺中预热石脑油的方法 |
| CN109957421B (zh) * | 2017-12-25 | 2021-01-01 | 中国石油天然气股份有限公司 | 一种催化裂化与轻烃深加工的组合方法 |
| US20200392055A1 (en) | 2018-02-22 | 2020-12-17 | Total Research & Technology Feluy | Improved Naphtha Steam Cracking Process |
| EP3830224A1 (fr) | 2018-07-27 | 2021-06-09 | SABIC Global Technologies B.V. | Procédé de production d'oléfines légères et de composés aromatiques à partir de naphta à point d'ébullition à coupe large |
| FR3104605B1 (fr) | 2019-12-16 | 2022-04-22 | Ifp Energies Now | Dispositif et procédé de production d’oléfines légères par craquage catalytique et vapocraquage. |
| FR3104604B1 (fr) * | 2019-12-16 | 2022-04-22 | Ifp Energies Now | Dispositif et procédé de production d’oléfines légères et d’aromatiques par craquage catalytique. |
| CN111704521B (zh) * | 2020-06-22 | 2021-10-26 | 中国科学院过程工程研究所 | 一种烯烃反应产物急冷处理系统和急冷处理方法 |
| KR20230058254A (ko) * | 2021-10-22 | 2023-05-03 | 서강대학교산학협력단 | 메탄의 직접 전환을 이용한 올레핀 제조 반응 장치 및 제조 공정 |
| CN116162012A (zh) * | 2021-11-25 | 2023-05-26 | 环球油品公司 | 从c4和/或c5烃生产乙烯和丙烯的集成方法 |
| CN114409492B (zh) * | 2021-12-15 | 2023-12-22 | 国家能源集团宁夏煤业有限责任公司 | 甲醇制低碳烯烃的装置及方法 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5028400A (en) * | 1987-04-29 | 1991-07-02 | Mobil Oil Corporation | Feedstock preparation and reactor system for conversion to oxygenates to olefins |
| JPH06166639A (ja) * | 1992-09-09 | 1994-06-14 | Tonen Chem Corp | 接触分解装置から副生する軽質ガスからのオレフィン類の回収方法 |
| US5523502A (en) * | 1993-11-10 | 1996-06-04 | Stone & Webster Engineering Corp. | Flexible light olefins production |
| CN1069682C (zh) * | 1997-12-23 | 2001-08-15 | 中国石油化工总公司 | 重油催化热裂解层柱粘土催化剂及其制备 |
| US6455750B1 (en) * | 1998-05-05 | 2002-09-24 | Exxonmobil Chemical Patents Inc. | Process for selectively producing light olefins |
| JP3707607B2 (ja) * | 1998-08-25 | 2005-10-19 | 旭化成ケミカルズ株式会社 | エチレンおよびプロピレンの製造方法 |
| US6602920B2 (en) * | 1998-11-25 | 2003-08-05 | The Texas A&M University System | Method for converting natural gas to liquid hydrocarbons |
| US6271433B1 (en) * | 1999-02-22 | 2001-08-07 | Stone & Webster Engineering Corp. | Cat cracker gas plant process for increased olefins recovery |
| US6441263B1 (en) * | 2000-07-07 | 2002-08-27 | Chevrontexaco Corporation | Ethylene manufacture by use of molecular redistribution on feedstock C3-5 components |
| DE10217866A1 (de) * | 2002-04-22 | 2003-11-06 | Linde Ag | Verfahren und Vorrichtung zur Olefinherstellung |
| US7128827B2 (en) * | 2004-01-14 | 2006-10-31 | Kellogg Brown & Root Llc | Integrated catalytic cracking and steam pyrolysis process for olefins |
| ES2913654T3 (es) * | 2004-03-08 | 2022-06-03 | China Petroleum & Chem Corp | Procedimiento de FCC con dos zonas de reacción |
| US20080081938A1 (en) * | 2006-09-28 | 2008-04-03 | Schultz Michael A | Absorption recovery processing of light olefins free of carbon dioxide |
-
2005
- 2005-10-07 KR KR1020050094467A patent/KR100632571B1/ko not_active Expired - Lifetime
-
2006
- 2006-05-19 JP JP2008534432A patent/JP5293954B2/ja active Active
- 2006-05-19 CN CN2006800269933A patent/CN101228104B/zh active Active
- 2006-05-19 BR BRPI0616497-8A patent/BRPI0616497B1/pt active IP Right Grant
- 2006-05-19 CA CA2617887A patent/CA2617887C/fr active Active
- 2006-05-19 WO PCT/KR2006/001880 patent/WO2007043738A1/fr not_active Ceased
- 2006-05-19 RU RU2008101551/04A patent/RU2416594C2/ru not_active Application Discontinuation
- 2006-05-19 EP EP06768537.0A patent/EP1931611A4/fr not_active Withdrawn
- 2006-06-01 US US11/421,496 patent/US7939702B2/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| RU2416594C2 (ru) | 2011-04-20 |
| JP5293954B2 (ja) | 2013-09-18 |
| CA2617887C (fr) | 2013-05-07 |
| JP2009511657A (ja) | 2009-03-19 |
| US7939702B2 (en) | 2011-05-10 |
| RU2008101551A (ru) | 2009-07-27 |
| CN101228104B (zh) | 2011-06-15 |
| KR100632571B1 (ko) | 2006-10-09 |
| US20070083071A1 (en) | 2007-04-12 |
| EP1931611A4 (fr) | 2017-03-15 |
| EP1931611A1 (fr) | 2008-06-18 |
| CN101228104A (zh) | 2008-07-23 |
| WO2007043738A1 (fr) | 2007-04-19 |
| CA2617887A1 (fr) | 2007-04-19 |
| BRPI0616497A2 (pt) | 2012-12-25 |
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